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HYDROCARBON REMOVAL FROM A VADOSE WELL <br /> SOP-25 <br /> Rev:JO'C <br /> POUNDS OF HYDROCARBON IN A VAPOR STREAM <br /> INPUT DATA: <br /> 1)Vapor flow rate acfm(usually by Pitot tube) <br /> 2)Vapor pressure at the flow measuring device(in inches of H2O)(use(-)for vacuum) <br /> 3)Vapor temperature at the flow-measuring device. <br /> 4)Hydrocarbon content of vapor(usually in mg/M)for ppmv you need molecular weight. <br /> 5)Length of time(usually hours)over which flow rate occurred) <br /> From periodic measurements, a calculation of total pounds of hydrocarbons removed from a well or from a system is <br /> calculated. The input data listed above are measured at a point in time. To calculate quantities removed, some <br /> assumptions must be made about what was happening between measurements. The following assumptions will be used for <br /> the sake of consistency: <br /> ASSUMPTIONS: <br /> 1)Vapor flow for the period equals the average of the initial and final reading for the period. <br /> 2) Pressure and temperature for the entire period will be the final reading. <br /> 3) Hydrocarbon concentration for the period equals the average of the initial and final reading. <br /> 4) The hours of operation can be taken from an hour meter, an electric meter or will be assumed to be equal to the time <br /> between measurements. <br /> 5) If the unit is found down-try to determine how many hours it did operate and use the data taken for the previous period to <br /> make the calculations. Restart the unit and then take data to start the next period. <br /> SAMPLE DATA AND CALCULATIONS <br /> Date Time Temp Press HC conc Vapor flow Calc. <br /> deg F in H2O mg/M3 acfm Ib. rem. <br /> 1/6/95 11:00 70 -46 2000 120 <br /> 1/7/95 13:00 55 -50 1350 90 <br /> 1/8/95 10:00 80 -13 750 100 7.4 <br /> Calculate the pounds of hydrocarbon removed from the system during the basis period from 13:00(1:00 pm)on the 7th to 10 <br /> am on the 8th. Pressure and temperature of the measurements(at the flow meter) must be corrected to the P and T used to <br /> report the HC concentration (which are P = 1 atm and T = 70 deg F). 1 atm = 14.7psia, 760 mm Hg, or 407 in H2O. Tabs = <br /> 460+T deg F <br /> Hours of operation = 21,T=80, P=-13, HC=(1350+750)/2 = 1050 mg/M3' Flow=95 <br /> (460+70) (407-13) 28.3 1050 1 <br /> 21 x 60 x 95 x ----------- x ------ x ------ x ------- x------ = 7.4 Ib <br /> (460+80) 407 1000 1000 454 <br /> hr min cu ft M3 g Ib ib <br /> ----- x----- x----- x Tcorr x PCorr x ------ x ------- x ------ _ ------- <br /> basis hr min cu ft M3 g basis <br /> 21 x 60 x 95 x 0.98 x 0.97 x 0.0283 x 1.050 x1/454 = 7.4 Ib. <br /> cumulative lbs. (the running total)=the sum of all the previous periods. <br /> Note: If results are given in ppm, an assumption about the molecular weight of the hydrocarbon must be made to convert <br /> ppm into mg/M3_ ppmv x molecular wt./24.1 = mg/M3. (Use 102 for gasoline) <br />